US3506244A - Mixing apparatus - Google Patents
Mixing apparatus Download PDFInfo
- Publication number
- US3506244A US3506244A US3506244DA US3506244A US 3506244 A US3506244 A US 3506244A US 3506244D A US3506244D A US 3506244DA US 3506244 A US3506244 A US 3506244A
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- United States
- Prior art keywords
- elements
- channels
- flow
- mixing
- channel
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-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
- B01F25/4321—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa the subflows consisting of at least two flat layers which are recombined, e.g. using means having restriction or expansion zones
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/8593—Systems
- Y10T137/87571—Multiple inlet with single outlet
- Y10T137/87652—With means to promote mixing or combining of plural fluids
Definitions
- This invention relates to mixing apparatus and in particular to the type of apparatus in which streams of fluid are divided into sub-streams and remixed, the operation being repeated until the desired degree of mixing is achieved.
- Such apparatus may for example have two channels in each element, each of which receives a portion of the flow from each channel of the next preceding element and each of which channels discharges into the next following element, dividing the flow of liquid therethrough between the two channels of that next following element.
- Such apparatus provides good flow mixing it a sufiiciently large number of elements are employed but, since the flow in one channel is, in effect, parallel to that in a second channel, no substantial shear forces are brought to bear. It is an object of this invention to provide an improved form of mixing apparatus which supplies shear mixing as well as flow mixing.
- apparatus for mixing liquids comprises a plurality of elements arranged end to end, each of which elements has an equal even number of channels passing therealong, the flow path of the liquid through each of which channels in one element being such that the liquid flow is divided between each of the channels in the next following element, whereby the liquid in the separate channels is mixed, and each of which elements the faces which cooperate with those of the next preceding element and the next following element are oblique to the general direction of liquid flow.
- each element has 2 channels where n is an integer greater than or equal to unity.
- each channel receives a proportion of the flow from each channel of the next preceding element and preferably the combined flow passes through a restricted throat, following which the channels open up again to divide the liquid flow between each of the channels in the the next following element. Continued repetition of these operations repeatedly splits the liquid flow and recombines it in other distributions, thus providing efiicient flow mixing.
- the construction of the present invention provides shear mixing in addition to flow mixing since the paths through which the separate liquid flows travel through the individual elements are unequal, due to the shape of the elements. Accordingly two notional points in two channels which have reached the same position in the direction of flow in one element do not reach the next element at the same time and travel through the elements in different times. Accordingly when they are reaching the point of recombination of the streams they do so with one lagging behind the other and this contributes to more efficient mixing. In some cases such notional points may catch up with one another at a later stage but the effect of the shear mixing combined with that of the flow mixing is suflicient to mix the two streams more thoroughly per element than has been achieved in the previously known mixers. In some assemblies a particularly advantageous arrangement may be one in which the elements are not arranged in a straight line but follow a curved path dictated by their shape. With such an arrangement the effect of shear mixing can be greater than with the straight arrangement.
- the elements may be made of any suitable material which is not attacked by the liquids being mixed.
- the elements may be constructed from metals such as iron, steel, brass or other suitable metal for the particular application.
- plastics materials such as rubber compositions, polyamides, polyacetals, polyphenylene oxides, polyvinyl chloride and polyolefins.
- FIGURE 1 is a projection in the vertical plane of one end view of an element of mixing apparatus according to the invention, which element has two flow channels,
- FIGURE 2 is a section along the line X-X in FIG- URE 1,
- FIGURE 3 is a projection in the vertical plane of the other end of the element
- FIGURE 4 is a section of similar character to the section in FIGURE 2 showing three elements arranged in a straight line, and
- FIGURE 5 is a section of similar character to that of FIGURE 2 showing three elements arranged to follow a curved path.
- a mixer element 1 has oblique faces 2 and 3 of equal and opposite inclinations to the flow of liquid through the channels 4 and 5 through the elements.
- the channels are divided at one end by a septum 6 (FIGURES 1 and 2) and at the other end by a septum 11 (FIGURE 3) which is at right angles to the septum 6.
- the channels 4 and 5 open out at one end by means of funnel-shaped sections 7 and 8 so that their openings at this end each occupy the whole of the area on one side of the septum 6.
- the channels 4 and open out at the other end by means of funnel-shaped sections' 9 and so that they each occupy the whole of the area on one side of the septum 11.
- next following element will be so arranged that the projection drawing, corresponding to FIGURE 1, of the next following element will be related to the projection drawing of FIGURE 1 as object and mirror image and this will therefore equally be true of the relationship between'the projection drawing of the upstream end of the next following element and the drawing of FIGURE 3.
- the next element in the series will be similar to that shown in the presentfigures and so alternately for as many elements as it is desired to use.
- FIGURE 4 three elements are shown, the first and third of which are identical with that shown in FIGURES 1, 2 and 3 and the second of which, designated 1, is an alternative type in which the projectional representations of the respective ends are related to those, of the elements designated 1 as object and mirror image. Similar relationships exist between the elements shown in FIGURE 5 although the actual shape of the elements designated 1 requires to be different from that used inthe arrangement of FIGURE 4. The flow paths and the projectional representations of the ends of the elements 1 are similar to those shown in FIGURES l to 3.
- Apparatus for mixing liquids which comprises a plurality of elements arranged end to end, each of which elements has an equal even number of channels passing therethrough, the flow pathof the liquid through each of which channels in one element being such that the liquid flow is divided between each of the channels in the next following element, whereby the liquid in the separate channels is mixed, and in each of which elements thefaces which cooperate with those of the next preceding element and the next following element are oblique to thements are arranged to follow a curved path.
- phenylene oxides polyvinyl chloride and polyolefins.
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Prostheses (AREA)
Description
April 14,1970 4, 51mm 3,505,244
' MIXING APPARATUS I Filed June 26, 1968 8 2 I f A x FIGJ F162 F/G.3
In uenlor ALASTAIR STRANG By DAVIS, HOXIE, FAITHFULL & HAPGOOD Attorneys United States Patent 3,506,244 MIXING APPARATUS Alastair Strang, Kenilworth, England, assignor to Cour taulds Limited, London, England, a British company Filed June 26, 1968, Ser. No. 740,216 Claims priority, application Great Britain, June 29, 1967, 30,075/ 67 Int. Cl. B01f 5/00 U.S. Cl. 259-4 7 Claims ABSTRACT OF THE DISCLOSURE Apparatus for mixing liquitls which comprises a plurality of elements arranged end to end, each of which elements has an equal even number of channels passing therethrough, the flow path of the liquid through each of which channels in one element being such that the liquid flow is divided between each of the channels in the next following element, whereby the liquid in the separate channels is mixed, and in each of which elements the faces which cooperate with those of the next preceding and next following elements are oblique to the general direction of liquid flow. Preferably the elements have 2. channels where n is an integer greater than or equal to unity.
This invention relates to mixing apparatus and in particular to the type of apparatus in which streams of fluid are divided into sub-streams and remixed, the operation being repeated until the desired degree of mixing is achieved.
It has been previously been proposed to provide apparatus in which a plurality of mixing elements are ar ranged end to end and cooperate with one another to provide channels through the elements which are arranged to cause mixing of liquids passing through the channels. Such apparatus may for example have two channels in each element, each of which receives a portion of the flow from each channel of the next preceding element and each of which channels discharges into the next following element, dividing the flow of liquid therethrough between the two channels of that next following element. Such apparatus provides good flow mixing it a sufiiciently large number of elements are employed but, since the flow in one channel is, in effect, parallel to that in a second channel, no substantial shear forces are brought to bear. It is an object of this invention to provide an improved form of mixing apparatus which supplies shear mixing as well as flow mixing.
According to the invention apparatus for mixing liquids comprises a plurality of elements arranged end to end, each of which elements has an equal even number of channels passing therealong, the flow path of the liquid through each of which channels in one element being such that the liquid flow is divided between each of the channels in the next following element, whereby the liquid in the separate channels is mixed, and each of which elements the faces which cooperate with those of the next preceding element and the next following element are oblique to the general direction of liquid flow.
Preferably each element has 2 channels where n is an integer greater than or equal to unity.
In each mixing element each channel receives a proportion of the flow from each channel of the next preceding element and preferably the combined flow passes through a restricted throat, following which the channels open up again to divide the liquid flow between each of the channels in the the next following element. Continued repetition of these operations repeatedly splits the liquid flow and recombines it in other distributions, thus providing efiicient flow mixing.
3,506,244 Patented Apr. 14, 1970 The upstream and downstream faces of each element, which cooperate with the downstream face of the next preceding element and the upstream face of the next following element, respectively, are oblique to the general direction of liquid flow. The inclination of the faces to the flow direction is not very critical although a sharp angle will provide better results than will a more obtuse angle. Conveniently the section through the elements in the plane through the longest and shortest lengths of the side wall may be in the form of a trapezium with equal angles at the ends of its parallel sides. In this form a number of elements may if desired be assembled together in a straight line. In other cases where a straight line formation is not required, equal and opposite inclinations of the two faces of the elements are not necessary, though they will in most cases be convenient.
The construction of the present invention provides shear mixing in addition to flow mixing since the paths through which the separate liquid flows travel through the individual elements are unequal, due to the shape of the elements. Accordingly two notional points in two channels which have reached the same position in the direction of flow in one element do not reach the next element at the same time and travel through the elements in different times. Accordingly when they are reaching the point of recombination of the streams they do so with one lagging behind the other and this contributes to more efficient mixing. In some cases such notional points may catch up with one another at a later stage but the effect of the shear mixing combined with that of the flow mixing is suflicient to mix the two streams more thoroughly per element than has been achieved in the previously known mixers. In some assemblies a particularly advantageous arrangement may be one in which the elements are not arranged in a straight line but follow a curved path dictated by their shape. With such an arrangement the effect of shear mixing can be greater than with the straight arrangement.
The elements may be made of any suitable material which is not attacked by the liquids being mixed. Thus in certain applications the elements may be constructed from metals such as iron, steel, brass or other suitable metal for the particular application. Alternatively they may be made from plastics materials such as rubber compositions, polyamides, polyacetals, polyphenylene oxides, polyvinyl chloride and polyolefins.
The invention will be further described, by way of example, with reference to the accompanying drawing, in which FIGURE 1 is a projection in the vertical plane of one end view of an element of mixing apparatus according to the invention, which element has two flow channels,
FIGURE 2 is a section along the line X-X in FIG- URE 1,
FIGURE 3 is a projection in the vertical plane of the other end of the element,
FIGURE 4 is a section of similar character to the section in FIGURE 2 showing three elements arranged in a straight line, and
FIGURE 5 is a section of similar character to that of FIGURE 2 showing three elements arranged to follow a curved path.
Referring to the drawing, a mixer element 1 has oblique faces 2 and 3 of equal and opposite inclinations to the flow of liquid through the channels 4 and 5 through the elements. The channels are divided at one end by a septum 6 (FIGURES 1 and 2) and at the other end by a septum 11 (FIGURE 3) which is at right angles to the septum 6. The channels 4 and 5 open out at one end by means of funnel-shaped sections 7 and 8 so that their openings at this end each occupy the whole of the area on one side of the septum 6. Similarly the channels 4 and open out at the other end by means of funnel-shaped sections' 9 and so that they each occupy the whole of the area on one side of the septum 11. If the direction of flow is assumed to be from left to right in FIGURE 2, in which the channel 5 is shown dotted for most of its length, the next following element will be so arranged that the projection drawing, corresponding to FIGURE 1, of the next following element will be related to the projection drawing of FIGURE 1 as object and mirror image and this will therefore equally be true of the relationship between'the projection drawing of the upstream end of the next following element and the drawing of FIGURE 3. The next element in the series will be similar to that shown in the presentfigures and so alternately for as many elements as it is desired to use.
Referring to FIGURE 4, three elements are shown, the first and third of which are identical with that shown in FIGURES 1, 2 and 3 and the second of which, designated 1, is an alternative type in which the projectional representations of the respective ends are related to those, of the elements designated 1 as object and mirror image. Similar relationships exist between the elements shown in FIGURE 5 although the actual shape of the elements designated 1 requires to be different from that used inthe arrangement of FIGURE 4. The flow paths and the projectional representations of the ends of the elements 1 are similar to those shown in FIGURES l to 3.
In operation liquid flows into channels 4 and 5 in the first element and on emergence from that element each flow is split into two passing over the septum 6 in the second element. In the second element part of the flow -in one element will divide its output between each of the channels in the next following element. Such multiple channel mixing elements have the advantage that they produce the same degree of mixing with a smaller number of elements. Thus a mixer consisting of x elements, with eight channels will divide the fiow into 8 streams, or 2 streams, so that a similar mixing effect is obtained as is provided by three times the number of two channel elements.
I claim:
1. Apparatus for mixing liquids 'which comprises a plurality of elements arranged end to end, each of which elements has an equal even number of channels passing therethrough, the flow pathof the liquid through each of which channels in one element being such that the liquid flow is divided between each of the channels in the next following element, whereby the liquid in the separate channels is mixed, and in each of which elements thefaces which cooperate with those of the next preceding element and the next following element are oblique to thements are arranged to follow a curved path. a
from the first channel and part of the flow from the second channel are combined together and flows down one channel of the second element while the remainder of each flow passes down the other channel of the second element. This operation is repeated for each element with the result that, for a given number of elements x, the number of different streams formed is 2 According to the position in the channels, the flow in one channel continually lags or leads the flow in the other channel by virtue of the shaping of the element, thus contributing shear mixing to the flow mixing previously referred to.
While the invention has been described and illustrated in the drawing with reference to two channel elements; it will be apparent that any even number of channels may be similarly arranged. In such a case each channel '6. Apparatus as claimed in claim 1 in which the elements are made of a metal.
7.' Apparatus as claimed in claim 1 in which the elements are made from plastics materials-including natural and synthetic rubber, polyamides, polyacetals, poly-;
phenylene oxides, polyvinyl chloride and polyolefins.
References Cited 1 in which each of
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB3007567A GB1220688A (en) | 1967-06-29 | 1967-06-29 | Mixing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3506244A true US3506244A (en) | 1970-04-14 |
Family
ID=10301876
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US3506244D Expired - Lifetime US3506244A (en) | 1967-06-29 | 1968-06-26 | Mixing apparatus |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US3506244A (en) |
| BE (1) | BE717340A (en) |
| DE (1) | DE1757880A1 (en) |
| FR (1) | FR1573407A (en) |
| GB (1) | GB1220688A (en) |
| NL (1) | NL6809073A (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3620506A (en) * | 1970-07-07 | 1971-11-16 | Fmc Corp | Fluid-mixing device |
| US4112520A (en) * | 1976-03-25 | 1978-09-05 | Oscar Patton Gilmore | Static mixer |
| US4222671A (en) * | 1978-09-05 | 1980-09-16 | Gilmore Oscar Patrick | Static mixer |
| US4573801A (en) * | 1983-03-02 | 1986-03-04 | Leschonski K | Apparatus for producing a gas solid two phase flow jet having a constant mass or volume flow rate and predetermined velocity |
| US5305823A (en) * | 1990-03-22 | 1994-04-26 | Valeo Thermique Habitacle | Zone controlled automobile air conditioning system with air mixers at selected outlets |
| US6190034B1 (en) * | 1995-10-03 | 2001-02-20 | Danfoss A/S | Micro-mixer and mixing method |
| US6274867B1 (en) * | 1998-09-28 | 2001-08-14 | Varian, Inc. | Multiple liquid flow electrospray interface |
| US20090044619A1 (en) * | 2007-08-13 | 2009-02-19 | Fiering Jason O | Devices and methods for producing a continuously flowing concentration gradient in laminar flow |
| US20090078614A1 (en) * | 2007-04-19 | 2009-03-26 | Mathew Varghese | Method and apparatus for separating particles, cells, molecules and particulates |
| US20100116657A1 (en) * | 2007-03-28 | 2010-05-13 | The Charles Stark Draper Laboratory, Inc. | Method and apparatus for concentrating molecules |
| US10611054B2 (en) * | 2014-09-03 | 2020-04-07 | Windmöller & Hölscher Kg | Overturning device for overturning molten material and purging method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3206170A (en) * | 1959-10-13 | 1965-09-14 | American Enka Corp | Mixing apparatus |
| US3239197A (en) * | 1960-05-31 | 1966-03-08 | Dow Chemical Co | Interfacial surface generator |
-
1967
- 1967-06-29 GB GB3007567A patent/GB1220688A/en not_active Expired
-
1968
- 1968-06-25 DE DE19681757880 patent/DE1757880A1/en active Pending
- 1968-06-26 US US3506244D patent/US3506244A/en not_active Expired - Lifetime
- 1968-06-27 NL NL6809073A patent/NL6809073A/xx unknown
- 1968-06-28 BE BE717340D patent/BE717340A/xx unknown
- 1968-07-01 FR FR1573407D patent/FR1573407A/fr not_active Expired
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3206170A (en) * | 1959-10-13 | 1965-09-14 | American Enka Corp | Mixing apparatus |
| US3239197A (en) * | 1960-05-31 | 1966-03-08 | Dow Chemical Co | Interfacial surface generator |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3620506A (en) * | 1970-07-07 | 1971-11-16 | Fmc Corp | Fluid-mixing device |
| US4112520A (en) * | 1976-03-25 | 1978-09-05 | Oscar Patton Gilmore | Static mixer |
| US4222671A (en) * | 1978-09-05 | 1980-09-16 | Gilmore Oscar Patrick | Static mixer |
| US4573801A (en) * | 1983-03-02 | 1986-03-04 | Leschonski K | Apparatus for producing a gas solid two phase flow jet having a constant mass or volume flow rate and predetermined velocity |
| US5305823A (en) * | 1990-03-22 | 1994-04-26 | Valeo Thermique Habitacle | Zone controlled automobile air conditioning system with air mixers at selected outlets |
| US6190034B1 (en) * | 1995-10-03 | 2001-02-20 | Danfoss A/S | Micro-mixer and mixing method |
| US6274867B1 (en) * | 1998-09-28 | 2001-08-14 | Varian, Inc. | Multiple liquid flow electrospray interface |
| US20100116657A1 (en) * | 2007-03-28 | 2010-05-13 | The Charles Stark Draper Laboratory, Inc. | Method and apparatus for concentrating molecules |
| US8679313B2 (en) | 2007-03-28 | 2014-03-25 | The Charles Stark Draper Laboratory, Inc. | Method and apparatus for concentrating molecules |
| US20090078614A1 (en) * | 2007-04-19 | 2009-03-26 | Mathew Varghese | Method and apparatus for separating particles, cells, molecules and particulates |
| US8292083B2 (en) | 2007-04-19 | 2012-10-23 | The Charles Stark Draper Laboratory, Inc. | Method and apparatus for separating particles, cells, molecules and particulates |
| US20090044619A1 (en) * | 2007-08-13 | 2009-02-19 | Fiering Jason O | Devices and methods for producing a continuously flowing concentration gradient in laminar flow |
| US7837379B2 (en) * | 2007-08-13 | 2010-11-23 | The Charles Stark Draper Laboratory, Inc. | Devices for producing a continuously flowing concentration gradient in laminar flow |
| US10611054B2 (en) * | 2014-09-03 | 2020-04-07 | Windmöller & Hölscher Kg | Overturning device for overturning molten material and purging method |
Also Published As
| Publication number | Publication date |
|---|---|
| FR1573407A (en) | 1969-07-04 |
| BE717340A (en) | 1968-12-02 |
| DE1757880A1 (en) | 1971-06-03 |
| NL6809073A (en) | 1968-12-30 |
| GB1220688A (en) | 1971-01-27 |
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